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Experimental and Mathematical Modelling of Factors Influencing Carbon Dioxide Absorption into the Aqueous Solution of Monoethanolamine and 1-Butyl-3-methylimidazolium Dibutylphosphate Using Response Surface Methodology (RSM)

This paper investigated the solubility of carbon dioxide (CO(2)) in an aqueous solution of monoethanolamine (MEA) and 1-butyl-3-methylimidazolium dibutylphosphate ((BMIM)(DBP)) ionic liquid (IL) hybrid solvents. Aqueous solutions of MEA-(BMIM)(DBP) hybrid solvents containing different concentrations...

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Detalles Bibliográficos
Autores principales: Azhar, Fatin Nor Arissa, Taha, Mohd Faisal, Mat Ghani, Siti Musliha, Ruslan, Muhammad Syafiq Hazwan, Md Yunus, Noor Mona
Formato: Online Artículo Texto
Lenguaje:English
Publicado: MDPI 2022
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC8953549/
https://www.ncbi.nlm.nih.gov/pubmed/35335143
http://dx.doi.org/10.3390/molecules27061779
Descripción
Sumario:This paper investigated the solubility of carbon dioxide (CO(2)) in an aqueous solution of monoethanolamine (MEA) and 1-butyl-3-methylimidazolium dibutylphosphate ((BMIM)(DBP)) ionic liquid (IL) hybrid solvents. Aqueous solutions of MEA-(BMIM)(DBP) hybrid solvents containing different concentrations of (BMIM)(DBP) were prepared to exploit the amine’s reactive nature, combined with the IL’s non-volatile nature for CO(2) absorption. Response surface methodology (RSM) based on central composite design (CCD) was used to design the CO(2) solubility experiments and to investigate the effects of three independent factors on the solubility of CO(2) in the aqueous MEA-(BMIM)(DBP) hybrid solvent. The three independent factors were the concentration of (BMIM)(DBP) (0–20 wt.%), temperature (30 °C–60 °C) and pressure of CO(2) (2–30 bar). The experimental data were fitted to a quadratic model with a coefficient of determination (R(2)) value of 0.9791. The accuracy of the developed model was confirmed through additional experiments where the experimental values were found to be within the 95% confidence interval. From the RSM-generated model, the optimum conditions for CO(2) absorption in aqueous 30 wt% MEA-(BMIM)(DBP) were 20 wt% of (BMIM)(DBP), a temperature of 41.1 °C and a pressure of 30 bar.